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WO2024185497A1 - Microsphères thermo-expansibles et leur utilisation - Google Patents

Microsphères thermo-expansibles et leur utilisation Download PDF

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Publication number
WO2024185497A1
WO2024185497A1 PCT/JP2024/006163 JP2024006163W WO2024185497A1 WO 2024185497 A1 WO2024185497 A1 WO 2024185497A1 JP 2024006163 W JP2024006163 W JP 2024006163W WO 2024185497 A1 WO2024185497 A1 WO 2024185497A1
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Prior art keywords
heat
expandable microspheres
weight
monomer
meth
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PCT/JP2024/006163
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English (en)
Japanese (ja)
Inventor
友洋 飯塚
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Matsumoto Yushi Seiyaku Co Ltd
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Matsumoto Yushi Seiyaku Co Ltd
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Priority to JP2024563518A priority Critical patent/JP7678944B2/ja
Priority to KR1020257032283A priority patent/KR20250162576A/ko
Priority to CN202480009338.5A priority patent/CN120548350A/zh
Priority to SE2550870A priority patent/SE2550870A1/en
Publication of WO2024185497A1 publication Critical patent/WO2024185497A1/fr
Anticipated expiration legal-status Critical
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/32—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof from compositions containing microballoons, e.g. syntactic foams
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/16—Making expandable particles
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00—Materials not provided for elsewhere
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02—Making microcapsules or microballoons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02—Making microcapsules or microballoons
    • B01J13/06—Making microcapsules or microballoons by phase separation
    • B01J13/14—Polymerisation; cross-linking

Definitions

  • the present invention relates to heat-expandable microspheres and their uses.
  • Heat-expandable microspheres are microspheres that have the characteristic of expanding when subjected to heat treatment. These heat-expandable microspheres are used in a wide range of applications, for example, when they are blended with a substrate. By heat treatment during molding, the heat-expandable microspheres expand simultaneously with molding, and can not only reduce the weight of the molded product but also impart design properties, cushioning properties, etc. to the molded product.
  • the thermoplastic resin used for the outer shell thereof is usually required to have gas barrier properties.
  • Patent Document 1 discloses thermally expandable microspheres in which the shell encapsulating a foaming agent can form a copolymer having a polymethacrylimide structure, and in particular, discloses a specific example of thermally expandable microspheres in which the monomers capable of forming the polymethacrylimide structure by copolymerization reaction are methacrylonitrile and methacrylic acid.
  • Patent Document 2 discloses heat-expandable microspheres having an outer shell made of a thermoplastic resin obtained by polymerizing a polymerizable component in which a methacrylate monomer and a carboxyl group-containing monomer are essential, and a nitrile monomer is contained in an amount of 0 to 30 parts by weight per 100 parts by weight of the total amount of the methacrylate monomer and the carboxyl group-containing monomer, and an encapsulated blowing agent which is essentially a hydrocarbon having 8 or more carbon atoms.
  • Patent Document 3 discloses heat-expandable microspheres which are hollow microparticles obtained by thermally expanding heat-expandable microspheres and which have a repeated high-temperature pressure resistance of 75% or more measured at 70°C and a blowing agent retention of 80% or more before and after the thermal expansion.
  • the thermally expandable microspheres disclosed in Patent Document 1 are excellent in heat resistance, have a high expansion ratio, and exhibit stable expansion behavior, the molded product obtained by using them is difficult to return to its original shape when it is deformed by the influence of external pressure.
  • the thermally expandable microspheres described in Patent Document 2 are almost spherical, have excellent expansion properties, and are easy to work with when mixed with a resin, but have insufficient expansion properties, and the molded product obtained by using them is difficult to return to its original shape when it is deformed by the influence of external pressure.
  • thermoly expandable microspheres disclosed in Patent Document 3 are nearly spherical in shape, have a uniform shell thickness, and are suppressed from having large resin particles on the inner side of the shell, but the molded product obtained by using them is difficult to return to its original shape when it is deformed by the influence of external pressure.
  • An object of the present invention is to provide heat-expandable microspheres which can give molded articles which are resistant to deformation over a long period of time, and uses thereof.
  • the present invention relates to heat-expandable microspheres which comprise an outer shell containing a thermoplastic resin and a blowing agent which is encapsulated in the outer shell and vaporizes when heated, wherein the thermoplastic resin is a polymer of a polymerizable component which contains at least one monomer selected from the group consisting of a carboxyl group-containing monomer, a (meth)acrylic acid ester monomer, a styrene monomer and a (meth)acrylamide monomer, and which have a recovery efficiency after compression of more than 0 and not more than 3.5 when heated for 2 minutes at a temperature 20° C. lower than the maximum expansion temperature of the heat-expandable microspheres and a compression recovery of 65% or more when heated for 2 minutes at a temperature 20° C. lower than the maximum expansion temperature of the heat-expandable microspheres.
  • the thermoplastic resin is a polymer of a polymerizable component which contains at least one monomer selected from the group consisting
  • the heat-expandable microspheres of the present invention preferably satisfy at least one of the following requirements 1) to 4).
  • the polymerizable component contains the carboxyl group-containing monomer and at least one monomer selected from the group consisting of the (meth)acrylic acid ester monomer, the styrene monomer, and the (meth)acrylamide monomer.
  • the weight ratio of the carboxyl group-containing monomer in the polymerizable component is 10 to 80% by weight, and the weight ratio of at least one monomer selected from the group consisting of the (meth)acrylic acid ester monomer, the styrene monomer, and the (meth)acrylamide monomer is 10 to 77% by weight.
  • the foaming agent contains 70% by weight or more of hydrocarbons having 5 to 6 carbon atoms.
  • the weight percentage of acrylonitrile in the polymerizable component is 13% by weight or less.
  • the hollow particles of the present invention are expanded products of the above-mentioned heat-expandable microspheres.
  • the fine particle-coated hollow particles of the present invention comprise the above-mentioned hollow particles and fine particles that are coated on the outer surface of the outer shell of the hollow particles.
  • the composition of the present invention contains at least one member selected from the group consisting of the above-mentioned heat-expandable microspheres, the above-mentioned hollow particles and the above-mentioned fine particle-coated hollow particles, and a base component.
  • the molded article of the present invention is produced by molding the above composition.
  • the heat-expandable microspheres of the present invention can produce molded products that are resistant to deformation over long periods of time.
  • the hollow particles of the present invention are lightweight and have excellent restoring properties.
  • the fine particle-coated hollow particles of the present invention are comprised of the above-mentioned hollow particles and fine particles that are adhered to the outer surface of the outer shell of the hollow particles, and are lightweight and have excellent restoring properties.
  • the composition of the present invention contains at least one selected from the group consisting of the heat-expandable microspheres, the hollow particles and the microparticle-coated hollow particles, and a base component, and can give molded articles which are lightweight and resistant to deformation over a long period of time.
  • the molded article of the present invention is obtained by molding the above composition, and is lightweight and resistant to deformation over a long period of time.
  • FIG. 1 is a schematic diagram showing an example of heat-expandable microspheres.
  • FIG. 2 is a schematic diagram showing an example of fine particle-adhered resin hollow particles.
  • the heat-expandable microspheres of the present invention comprise a shell containing a thermoplastic resin and a blowing agent encapsulated in the shell and vaporized by heating, and the microspheres as a whole exhibit heat expandability (the property that the entire microsphere expands when heated).
  • the heat-expandable microspheres of the present invention have a core-shell structure composed of an outer shell 6 and a foaming agent (core) 7 .
  • the thermoplastic resin that forms the outer shell of the heat-expandable microspheres of the present invention is a polymer of a polymerizable component.
  • the polymerizable component includes a monomer having one (radical) polymerizable carbon-carbon double bond, and the monomer having one (radical) polymerizable carbon-carbon double bond is a component capable of undergoing an addition reaction.
  • the polymerizable component includes at least one selected from a carboxyl group-containing monomer, a (meth)acrylic acid ester monomer, a styrene monomer, and a (meth)acrylamide monomer.
  • the carboxyl group-containing monomer, the (meth)acrylic acid ester monomer, the styrene monomer, and the (meth)acrylamide monomer include a monomer having one (radically) polymerizable carbon-carbon double bond.
  • the heat-expandable microspheres of the present invention have a recovery efficiency after compression of more than 0 and not more than 3.5 when heated for 2 minutes at a temperature 20°C lower than their maximum expansion temperature, and a compression recovery of 65% or more when heated for 2 minutes at a temperature 20°C lower than their maximum expansion temperature.
  • Such heat-expandable microspheres provide an outer shell that is highly heat resistant and flexible, and the resulting expanded body can be subjected to high internal pressure, which is thought to suppress deformation due to external forces and, even if deformation occurs, quickly restores the original shape, thereby providing a molded product that is resistant to deformation over a long period of time.
  • Carboxyl group-containing monomers are not particularly limited, but examples include unsaturated monocarboxylic acids such as acrylic acid, methacrylic acid, ethacrylic acid, crotonic acid, and cinnamic acid; unsaturated dicarboxylic acids such as maleic acid, itaconic acid, fumaric acid, citraconic acid, and chloromaleic acid; anhydrides of unsaturated dicarboxylic acids; unsaturated dicarboxylic acid monoesters such as monomethyl maleate, monoethyl maleate, monobutyl maleate, monomethyl fumarate, monoethyl fumarate, monomethyl itaconate, monoethyl itaconate, and monobutyl itaconate, and these monomers may be used alone or in combination of two or more. In addition, some or all of the carboxyl groups of the monomers may be neutralized during or after polymerization, or may be in the form of a salt.
  • unsaturated monocarboxylic acids such as
  • the (meth)acrylic acid ester monomer is not particularly limited, and examples thereof include methyl (meth)acrylate, ethyl (meth)acrylate, n-butyl (meth)acrylate, t-butyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, stearyl (meth)acrylate, phenyl (meth)acrylate, isobornyl (meth)acrylate, cyclohexyl (meth)acrylate, benzyl (meth)acrylate, and 2-hydroxyethyl (meth)acrylate, and these monomers may be used alone or in combination of two or more.
  • acrylic acid and methacrylic acid may be collectively referred to as (meth)acrylic acid.
  • (meth)acrylate means acrylate or methacrylate
  • (meth)acrylic means acrylic or methacrylic.
  • the styrene monomer is not particularly limited, but examples thereof include styrene, ⁇ -methylstyrene, styrenesulfonic acid and its salts, and these styrene monomers may be used alone or in combination of two or more.
  • examples of the (meth)acrylamide monomer include acrylamide, substituted acrylamide, methacrylamide, and substituted methacrylamide. These monomers may be used alone or in combination of two or more.
  • the weight percentage of the total of the carboxyl group-containing monomer, the (meth)acrylic acid ester monomer, the styrene monomer, and the (meth)acrylamide monomer in the polymerizable components is not particularly limited, but is preferably 20 to 100% by weight. When the weight percentage is within the above range, the heat resistance of the shell is improved, and the shell tends to have good flexibility. Furthermore, yellowing during heating tends to be reduced.
  • the upper limit of the weight percentage is more preferably 99.99% by weight, and even more preferably 99.98% by weight.
  • the lower limit of the weight percentage is more preferably 25% by weight, and even more preferably 30% by weight.
  • the weight percentage is, for example, more preferably 25 to 99.99% by weight, and even more preferably 30 to 99.98% by weight.
  • the weight ratio of the carboxyl group-containing monomer in the polymerizable component is not particularly limited, but is preferably 10 to 80% by weight. If the weight ratio is 10% by weight or more, the heat resistance of the shell tends to improve, and the recovery tends to improve. On the other hand, if the weight ratio is 80% by weight or less, the rigidity of the shell tends not to be too high, and tends to be in a moderate state.
  • the upper limit of the weight ratio is more preferably 75% by weight, even more preferably 70% by weight, particularly preferably 65% by weight, and most preferably 60% by weight.
  • the lower limit of the weight ratio is more preferably 14% by weight, and even more preferably 18% by weight.
  • the weight ratio is, for example, more preferably 14 to 70% by weight, and even more preferably 18 to 65% by weight.
  • the polymerizable component is not particularly limited, but if it contains a carboxyl group-containing monomer and further contains at least one monomer selected from a (meth)acrylic acid ester monomer, a styrene monomer, and a (meth)acrylamide monomer, it is preferable in that it improves heat resistance and improves the restorability of the resulting expanded body, and is also preferable in that it reduces yellowing when heated.
  • the weight ratio of the at least one selected from a (meth)acrylic acid ester monomer, a styrene monomer, and a (meth)acrylamide is preferably 10 to 77% by weight.
  • the weight ratio is 10% by weight or more, the heat resistance of the shell tends to improve and the recovery tends to improve. Also, yellowing during heating tends to be reduced.
  • the weight ratio when the weight ratio is 77% by weight or less, the rigidity of the shell tends not to be too high and tends to be in a moderate state.
  • the upper limit of the weight ratio is more preferably 65% by weight, even more preferably 55% by weight, and particularly preferably 45% by weight.
  • the lower limit of the weight ratio is more preferably 12% by weight, and even more preferably 14% by weight.
  • the weight ratio is, for example, more preferably 12 to 70% by weight, and even more preferably 14 to 65% by weight.
  • the weight percentage of acrylonitrile in the polymerizable component is not particularly limited, but is preferably 13% by weight or less. When the weight percentage is 13% by weight or less, the outer shell has an appropriate rigidity, and the resulting expanded body tends to have improved resilience to external forces. Also, yellowing during heating tends to be reduced.
  • the upper limit of the weight percentage is more preferably 10% by weight, even more preferably 7% by weight, and particularly preferably 5% by weight.
  • the lower limit of the weight percentage is preferably 0% by weight.
  • the weight percentage may be, for example, more preferably 0 to 10% by weight, and even more preferably 0 to 7% by weight.
  • the polymerizable component may contain, in addition to the above-mentioned acrylonitrile, carboxyl group-containing monomer, (meth)acrylic acid ester monomer, styrene monomer, and (meth)acrylamide monomer, a monomer having one (radically) polymerizable carbon-carbon double bond (hereinafter, sometimes simply referred to as other monomer).
  • Examples of the other monomer components include nitrile monomers other than acrylonitrile, such as methacrylonitrile, fumaronitrile, and maleonitrile; halogenated vinyl monomers, such as vinyl chloride; halogenated vinylidene monomers, such as vinylidene chloride; vinyl ester monomers, such as vinyl acetate, vinyl propionate, and vinyl butyrate; ethylenically unsaturated monoolefin monomers, such as ethylene, propylene, and isobutylene; vinyl ether monomers, such as vinyl methyl ether, vinyl ethyl ether, and vinyl isobutyl ether; vinyl ketone monomers, such as vinyl methyl ketone; N-vinyl monomers, such as N-vinyl carbazole and N-vinyl pyrrolidone; and vinyl naphthalene salts. These other monomer components may be used alone or in combination of two or more.
  • the polymerizable component is not particularly limited, but may contain methacrylonitrile.
  • the weight percentage of methacrylonitrile in the polymerizable component is not particularly limited, but is preferably 0 to 70% by weight.
  • the upper limit of the weight percentage is more preferably 65% by weight, even more preferably 60% by weight, and particularly preferably 55% by weight.
  • the lower limit of the weight percentage is more preferably 5% by weight, even more preferably 10% by weight, and particularly preferably 15% by weight.
  • the weight percentage is, for example, more preferably 0 to 65% by weight, and more preferably 5 to 60% by weight.
  • the polymerizable component may contain a monomer having at least two (radically) polymerizable carbon-carbon double bonds (hereinafter, sometimes simply referred to as a crosslinking agent) in addition to the above-mentioned monomer having one (radically) polymerizable carbon-carbon double bond.
  • the crosslinking agent is also a component capable of an addition reaction, and the resulting thermoplastic resin can have a crosslinked structure.
  • the resulting heat-expandable microspheres tend to suppress a decrease in the retention rate (encapsulation retention rate) of the encapsulated blowing agent during thermal expansion.
  • Crosslinking agents include, for example, aromatic divinyl compounds such as divinylbenzene; allyl methacrylate, triacrylformal, triallyl isocyanate, ethylene glycol di(meth)acrylate, diethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, neopentyl glycol di(meth)acrylate, polytetramethylene glycol diacrylate, 1,4-butanediol di(meth)acrylate, 1,6-hexanediol di(meth)acrylate, 1,9-nonanediol di(meth)acrylate, P
  • polyfunctional (meth)acrylate compounds include EG#200 di(meth)acrylate, PEG#400 di(meth)acrylate, PEG#600 di(meth)acrylate, trimethylolpropane tri(meth)acrylate, pentaerythritol tri(meth)acrylate, pentaerythrito
  • the polymerizable component does not have to contain a crosslinking agent, but there is no particular limit to the amount of the crosslinking agent.
  • the amount is preferably 0 to 4% by weight, more preferably 0.01 to 2% by weight, even more preferably 0.02 to 1% by weight, and particularly preferably 0.05 to 0.5% by weight, based on 100% by weight of the polymerizable component.
  • the blowing agent contained in the heat-expandable microspheres of the present invention is a component that vaporizes when heated.
  • the blowing agent is encapsulated in the outer shell of the heat-expandable microspheres, so that the heat-expandable microspheres as a whole exhibit heat expandability (the property that the whole microsphere expands when heated).
  • the foaming agent is not particularly limited, and examples thereof include propane, butane, isobutane, n-pentane, 2-methylbutane, 2,2-dimethylpropane, cyclopentane, n-hexane, 2-methylpentane, 3-methylpentane, 2,2-dimethylbutane, 2,3-dimethylbutane, heptane, isoheptane, octane, isooctane, nonane, isononane, decane, isodecane, dodecane, isododecane, tridecane, isotridecane, 4-methyldodecane, tetradecane, isotetradecane, pentadecane, isopentadecane, hexadecane, isohexadecane, 2,2,4,4,6,8,8-heptamethylnonane, heptadecane, iso Examples of such
  • the foaming agent there are no particular limitations on the foaming agent, but it is preferable for the foaming agent to contain a hydrocarbon having 5 to 6 carbon atoms, as this provides a good balance with the heat resistance of the outer shell and improves the restorability of the resulting expanded body when it is deformed.
  • the weight ratio of the hydrocarbons having 5 to 6 carbon atoms in the blowing agent is not particularly limited, but is preferably 70% by weight or more.
  • the lower limit of the weight ratio is more preferably 75% by weight or more, even more preferably more than 80% by weight, particularly preferably more than 85% by weight, and most preferably 90% by weight or more.
  • the upper limit of the weight ratio is preferably 100% by weight.
  • the blowing agent may be composed only of hydrocarbons having 5 to 6 carbon atoms. Furthermore, when the foaming agent contains a hydrocarbon having 5 carbon atoms or a hydrocarbon having 6 carbon atoms, the weight ratio of the hydrocarbon having 5 carbon atoms or the hydrocarbon having 6 carbon atoms in the foaming agent should be within the above range.
  • the weight ratio of the hydrocarbon with 5 carbon atoms to the hydrocarbon with 6 carbon atoms is not particularly limited, but is preferably 55/45 to 90/10.
  • the upper limit of the weight ratio is more preferably 85/15, and even more preferably 80/20.
  • the lower limit of the weight ratio is more preferably 58/42, and even more preferably 60/40.
  • the weight ratio is, for example, more preferably 58/42 to 85/15, and even more preferably 60/40 to 80/20.
  • the content of the blowing agent encapsulated in the heat-expandable microspheres of the present invention is defined as the percentage of the weight of the blowing agent encapsulated in the heat-expandable microspheres to the weight of the heat-expandable microspheres themselves.
  • the content is not particularly limited, but is preferably 5 to 50% by weight. When the content is 5% by weight or more, the expansion performance of the heat-expandable microspheres tends to be improved. On the other hand, when the content is 50% by weight or less, the heat resistance tends to be improved.
  • the upper limit of the content is more preferably 40% by weight, further preferably 35% by weight, and particularly preferably 30% by weight. On the other hand, the lower limit of the content is more preferably 7% by weight, and further preferably 10% by weight.
  • the content is, for example, more preferably 7 to 40% by weight, and further preferably 10 to 30% by weight.
  • the heat-expandable microspheres of the present invention have a recovery efficiency after compression of more than 0 and not more than 3.5 when heated for 2 minutes at a temperature 20° C. lower than their maximum expansion temperature, and a compression recovery of 65% or more when heated for 2 minutes at a temperature 20° C. lower than their maximum expansion temperature. If the heat-expandable microspheres of the present invention do not satisfy the above-mentioned restoring efficiency and compression recovery, the expanded body obtained as the processed product will be deformed by an external force.
  • the heat-expandable microspheres of the present invention preferably have a restoration efficiency after compression when heated for 2 minutes at a temperature 20°C lower than their maximum expansion temperature of 3.1, more preferably 2.7, and even more preferably 2.4.
  • the lower limit of the restoration efficiency is preferably 0.5, more preferably 1.0.
  • the restoration efficiency is, for example, preferably 0.5 to 3.1, and more preferably 1.0 to 2.7.
  • the recovery efficiency after compression when heated for 2 minutes at a temperature 20° C. lower than the maximum expansion temperature of the heat-expandable microspheres is measured by the method described in the Examples, and is expressed in units of MPa/mm.
  • the heat-expandable microspheres of the present invention preferably have a compression recovery of 70 to 100%, more preferably 75 to 100%, when heated for 2 minutes at a temperature 20° C. lower than their maximum expansion temperature.
  • the compression recovery when the heat-expandable microspheres are heated for 2 minutes at a temperature 20° C. lower than the maximum expansion temperature thereof is measured by the method described in the Examples.
  • the expansion start temperature (Ts) of the heat-expandable microspheres of the present invention is not particularly limited, but is preferably 100 to 200°C.
  • the upper limit of the expansion start temperature is more preferably 190°C, even more preferably 180°C, particularly preferably 170°C, and most preferably 160°C.
  • the lower limit of the expansion start temperature is more preferably 110°C, even more preferably 120°C, and particularly preferably 130°C.
  • the expansion start temperature is, for example, more preferably 110 to 180°C, and even more preferably 130 to 170°C.
  • the maximum expansion temperature (Tmax) of the heat-expandable microspheres of the present invention is not particularly limited, but is preferably 140 to 300°C. When the maximum expansion temperature is 140°C or higher, sufficient heat resistance tends to be obtained. On the other hand, when the maximum expansion temperature is 300°C or lower, expansion performance tends to be improved.
  • the upper limit of the maximum expansion temperature is more preferably 250°C, further preferably 220°C, and particularly preferably 210°C.
  • the lower limit of the maximum expansion temperature is more preferably 150°C, and further preferably 160°C.
  • the maximum expansion temperature is, for example, more preferably 150 to 250°C, and further preferably 160 to 210°C.
  • the expansion starting temperature (Ts) and maximum expansion temperature (Tmax) of the heat-expandable microspheres are measured by the methods described in the Examples.
  • the average particle size of the heat-expandable microspheres of the present invention is not particularly limited, but is preferably 1 to 200 ⁇ m. When the average particle size is 1 ⁇ m or more, the expansion performance of the heat-expandable microspheres tends to be improved. On the other hand, when the average particle size is 200 ⁇ m or less, the heat resistance tends to be improved.
  • the upper limit of the average particle size is more preferably 80 ⁇ m, further preferably 50 ⁇ m, and particularly preferably 40 ⁇ m.
  • the lower limit of the average particle size is more preferably 5 ⁇ m, and further preferably 10 ⁇ m.
  • the average particle size is, for example, more preferably 5 to 80 ⁇ m, and further preferably 10 to 50 ⁇ m.
  • the average particle size of the heat-expandable microspheres is measured by the method described in the Examples.
  • the coefficient of variation CV of the particle size distribution of the heat-expandable microspheres of the present invention is not particularly limited, but is preferably 50% or less, more preferably 40% or less, even more preferably 35% or less, and particularly preferably 30% or less.
  • the coefficient of variation CV of the particle size distribution of the heat-expandable microspheres is calculated by the following formulas (1) and (2).
  • s is the standard deviation of the particle diameters
  • ⁇ x> is the average particle diameter
  • xi is the i-th particle diameter
  • n is the number of particles.
  • the maximum expansion ratio of the heat-expandable microspheres of the present invention is not particularly limited, but is preferably 10 times or more, more preferably 15 times or more, even more preferably 20 times or more, particularly preferably 30 times or more, and even more preferably 50 times or more.
  • the upper limit of the maximum expansion ratio is preferably 300 times.
  • the method for producing heat-expandable microspheres of the present invention comprises the steps of dispersing an oily mixture containing a polymerizable component, a blowing agent, and a polymerization initiator in an aqueous dispersion medium and polymerizing the polymerizable component (hereinafter, sometimes simply referred to as a polymerization step).
  • the polymerization initiator is not particularly limited, but examples thereof include peroxides and azo compounds.
  • peroxides include peroxydicarbonates such as diisopropyl peroxydicarbonate, di-sec-butyl peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, and dibenzyl peroxydicarbonate; diacyl peroxides such as dilauroyl peroxide and dibenzoyl peroxide; ketone peroxides such as methyl ethyl ketone peroxide and cyclohexanone peroxide; peroxy ketals such as 2,2-bis(t-butylperoxy)butane; hydroperoxides such as cumene hydroperoxide and t-butyl hydroperoxide; dialkyl peroxides such as dicumyl peroxide and di-t-butyl peroxide; and peroxy esters such as t-hexyl peroxypivalate
  • azo compounds examples include 2,2'-azobis(4-methoxy-2,4-dimethylvaleronitrile), 2,2'-azobisisobutyronitrile, 2,2'-azobis(2,4-dimethylvaleronitrile), 2,2'-azobis(2-methylpropionate), 2,2'-azobis(2-methylbutyronitrile), and 1,1'-azobis(cyclohexane-1-carbonitrile).
  • the amount of the polymerization initiator is not particularly limited, but is preferably 0.05 to 15 parts by weight, more preferably 0.1 to 10 parts by weight, and most preferably 0.3 to 5 parts by weight, per 100 parts by weight of the polymerizable component. When the amount used is within the above range, the heat resistance and expansion performance of the resulting heat-expandable microspheres tend to be improved.
  • the aqueous dispersion medium is a medium for dispersing the oily mixture essentially consisting of the polymerizable component and the blowing agent, and is mainly composed of water such as ion-exchanged water.
  • the aqueous dispersion medium may further contain alcohol such as methanol, ethanol, propanol, etc., or a hydrophilic organic solvent such as acetone.
  • hydrophilicity means a state in which it can be arbitrarily mixed with water.
  • the amount of the aqueous dispersion medium used but it is preferable to use 100 to 1,000 parts by weight of the aqueous dispersion medium per 100 parts by weight of the polymerizable component.
  • the aqueous dispersion medium may further contain an electrolyte.
  • the electrolyte include sodium chloride, magnesium chloride, calcium chloride, sodium sulfate, magnesium sulfate, ammonium sulfate, sodium carbonate, etc. These electrolytes may be used alone or in combination of two or more. When an electrolyte is used, its amount is not particularly limited, but is preferably 0.1 to 50 parts by weight based on 100 parts by weight of the aqueous dispersion medium.
  • the aqueous dispersion medium may contain at least one water-soluble compound selected from polyalkyleneimines having a structure in which an alkyl group substituted with a hydrophilic functional group selected from a carboxylic acid (salt) group and a phosphonic acid (salt) group is bonded to a nitrogen atom, water-soluble 1,1-substituted compounds having a structure in which a hydrophilic functional group selected from a hydroxyl group, a carboxylic acid (salt) group, and a phosphonic acid (salt) group and a hetero atom are bonded to the same carbon atom, potassium dichromate, alkali metal nitrite, metal (III) halides, boric acid, water-soluble ascorbic acids, water-soluble polyphenols, water-soluble vitamin Bs, and water-soluble phosphonic acids (salts).
  • water-soluble means that 1 g or more of the substance dissolves in 100 g of water.
  • the amount of the water-soluble compound contained in the aqueous dispersion medium is not particularly limited, but is preferably 0.0001 to 1.0 parts by weight, more preferably 0.0003 to 0.1 parts by weight, and particularly preferably 0.001 to 0.05 parts by weight, per 100 parts by weight of the polymerizable component. If the amount of the water-soluble compound is too small, the effect of the water-soluble compound may not be fully obtained. Also, if the amount of the water-soluble compound is too large, the polymerization rate may decrease or the amount of the polymerizable component (raw material) remaining may increase.
  • the aqueous dispersion medium may contain a dispersion stabilizer or a dispersion stabilization assistant in addition to the electrolyte and the water-soluble compound.
  • a dispersion stabilizer examples include tribasic calcium phosphate, magnesium pyrophosphate obtained by a double decomposition method, calcium pyrophosphate, colloidal silica, alumina sol, magnesium hydroxide, etc. These dispersion stabilizers may be used alone or in combination of two or more kinds.
  • the amount of the dispersion stabilizer is preferably 0.05 to 30 parts by weight, more preferably 0.2 to 20 parts by weight, based on 100 parts by weight of the polymerizable component.
  • the dispersion stabilization aid is not particularly limited, but examples include polymer-type dispersion stabilization aids, cationic surfactants, anionic surfactants, zwitterionic surfactants, nonionic surfactants, and other surfactants. These dispersion stabilization aids may be used alone or in combination of two or more kinds.
  • the aqueous dispersion medium is prepared, for example, by mixing water (ion-exchanged water) with a water-soluble compound and, if necessary, a dispersion stabilizer or a dispersion stabilization assistant.
  • the pH of the aqueous dispersion medium during polymerization is appropriately determined depending on the type of water-soluble compound, dispersion stabilizer, and dispersion stabilization assistant.
  • the polymerization may be carried out in the presence of sodium hydroxide and/or zinc chloride.
  • an oily mixture is suspended and dispersed in an aqueous dispersion medium so as to prepare spherical oil droplets having a predetermined particle size.
  • a chain transfer agent, an organic pigment, an inorganic pigment or inorganic particles whose surface has been treated to be hydrophobic, or the like may be further used.
  • the oily mixture is suspended and dispersed in an aqueous dispersion medium so as to prepare spherical oil droplets having a predetermined particle size.
  • methods for suspending and dispersing the oily mixture include general dispersion methods such as stirring with a homomixer (e.g., manufactured by Primix Corporation) or the like, a method using a static dispersion device such as a static mixer (e.g., manufactured by Noritake Co., Ltd.), a membrane emulsification method, and an ultrasonic dispersion method.
  • the aqueous suspension in which the oily mixture is dispersed in the aqueous dispersion medium as oil globules is then heated to initiate suspension polymerization.
  • the aqueous suspension is preferably stirred, and the stirring may be carried out gently enough to prevent the floating of the monomer components and the settling of the heat-expandable microspheres after polymerization.
  • the polymerization temperature can be freely set depending on the type of polymerization initiator, but is preferably controlled in the range of 30 to 100°C, and more preferably 40 to 90°C.
  • the reaction temperature is preferably maintained for about 0.1 to 20 hours.
  • the obtained slurry is filtered using a centrifuge, a pressure press, a vacuum dehydrator, or the like to obtain a wet powder having a moisture content of 10 to 50% by weight, preferably 15 to 45% by weight, and more preferably 20 to 40% by weight.
  • the obtained wet powder is then dried using a tray dryer, an indirect heating dryer, a fluidized bed dryer, a vacuum dryer, a vibration dryer, an airflow dryer, or the like to obtain a dry powder.
  • the moisture content of the obtained dry powder is preferably 8% by weight or less, and more preferably 5% by weight or less.
  • the obtained wet powder or dry powder may be washed with water and/or redispersed, filtered again, and dried.
  • the slurry may be dried using a spray dryer, fluidized bed dryer, or the like to obtain a dry powder.
  • the wet powder and dry powder may be appropriately selected depending on the intended use.
  • the hollow particles of the present invention are particles obtained by heating and expanding the above-described heat-expandable microspheres.
  • the hollow particles of the present invention are lightweight and have excellent material properties when incorporated into compositions or molded products.
  • the hollow particles of the present invention are obtained by heating and expanding the heat-expandable microspheres described above, preferably at 80 to 450°C.
  • a dry heat expansion method is the method described in JP-A-2006-213930, particularly the internal injection method.
  • Another example of a dry heat expansion method is the method described in JP-A-2006-96963.
  • An example of a wet heat expansion method is the method described in JP-A-62-201231.
  • the average particle size of the hollow particles of the present invention is not particularly limited, but can be freely designed depending on the application, and is preferably 3 to 1000 ⁇ m, more preferably 10 to 500 ⁇ m, further preferably 15 to 300 ⁇ m, and particularly preferably 30 to 300 ⁇ m.
  • the coefficient of variation CV of the particle size distribution of the hollow particles of the present invention is not particularly limited, but is preferably 50% or less, more preferably 40% or less, further preferably 35% or less, and particularly preferably 30% or less.
  • the true specific gravity of the hollow particles of the present invention is preferably 0.001 to 0.60, more preferably 0.002 to 0.50, even more preferably 0.003 to 0.40, particularly preferably 0.004 to 0.30, and most preferably 0.005 to 0.20.
  • the fine particle-coated hollow particle of the present invention includes the above-described hollow particle and fine particles attached to the outer surface of the outer shell of the hollow particle.
  • the outer surface of the outer shell of the hollow particle is formed of fine particles (4 and 5) attached to the outer surface of the outer shell (2).
  • the term "attached” as used herein may simply mean that the fine particles 4 and 5 are adsorbed on the outer surface of the outer shell 2 of the hollow particle (as in the state of the fine particle 4 in FIG.
  • thermoplastic resin constituting the hollow particle may be melted by heating, and the fine particles may be embedded in the outer surface of the shell of the hollow particle and fixed therein (the state of the fine particles 5 in FIG. 2).
  • the shape may be irregular or spherical.
  • fine particles can be used, and may be made of either inorganic or organic materials.
  • the shape of the fine particles may be spherical, needle-like, plate-like, or the like.
  • the inorganic substance constituting the fine particles is not particularly limited, but examples thereof include wollastonite, sericite, kaolin, mica, clay, talc, bentonite, alumina silicate, pyrophyllite, montmorillonite, calcium silicate, calcium carbonate, magnesium carbonate, dolomite, calcium sulfate, barium sulfate, glass flakes, boron nitride, silicon carbide, silica, alumina, mica, titanium dioxide, zinc oxide, magnesium oxide, zinc oxide, hydrosaltite, carbon black, molybdenum disulfide, tungsten disulfide, ceramic beads, glass beads, quartz beads, glass microballoons, and the like.
  • the organic matter constituting the fine particles is not particularly limited, and examples thereof include sodium carboxymethylcellulose, hydroxyethylcellulose, methylcellulose, ethylcellulose, nitrocellulose, hydroxypropylcellulose, sodium alginate, polyvinyl alcohol, polyvinylpyrrolidone, sodium polyacrylate, carboxyvinyl polymer, polyvinyl methyl ether, magnesium stearate, calcium stearate, zinc stearate, polyethylene wax, lauric acid amide, myristic acid amide, palmitic acid amide, stearic acid amide, hydrogenated castor oil, (meth)acrylic resin, polyamide resin, silicone resin, urethane resin, polyethylene resin, polypropylene resin, and fluorine-based resin.
  • the inorganic or organic matter constituting the fine particles may be treated with a surface treatment agent such as a silane coupling agent, paraffin wax, fatty acid, resin acid, urethane compound, or fatty acid ester, or may be untreated
  • the average particle size of the fine particles is not particularly limited, but is preferably 0.001 to 30 ⁇ m, more preferably 0.005 to 25 ⁇ m, and particularly preferably 0.01 to 20 ⁇ m.
  • the average particle size is the cumulative 50% particle size on a volume basis measured by a laser diffraction method.
  • the ratio of the average particle size of fine particles to the average particle size of hollow particles is not particularly limited, but from the viewpoint of the adhesion of the fine particles to the surfaces of the hollow particles, it is preferably 1 or less, more preferably 0.1 or less, and even more preferably 0.05 or less.
  • the weight ratio of the fine particles to the entire fine particle-adhered hollow particles is preferably 10 to 95% by weight, more preferably 20 to 90% by weight or less, even more preferably 30 to 85% by weight, and particularly preferably 40 to 80% by weight. If the weight ratio is within the above range, the effect of adhering the fine particles tends to be improved.
  • the true specific gravity of the fine particle-coated hollow particles is not particularly limited, but is preferably 0.01 to 0.60, more preferably 0.03 to 0.40, even more preferably 0.05 to 0.30, and particularly preferably 0.07 to 0.20.
  • the method for producing the microparticle-coated hollow particles of the present invention can be, for example, by heating and expanding microparticle-coated heat-expandable microspheres.
  • a preferred method for producing microparticle-coated hollow particles includes a step of mixing heat-expandable microspheres with microparticles (mixing step), and a step of heating the mixture obtained in the mixing step to a temperature above the softening point to expand the heat-expandable microspheres and to cause microparticles to adhere to the outer surfaces of the obtained hollow particles (adhering step).
  • the mixing step is a step in which the heat-expandable microspheres and the fine particles are mixed together.
  • the weight ratio of the fine particles to the total weight of the heat-expandable microspheres and fine particles in the mixing step is not particularly limited, but is preferably 10 to 95% by weight, more preferably 20 to 90% by weight, further preferably 30 to 85% by weight, and particularly preferably 40 to 80% by weight.
  • the device used to mix the heat-expandable microspheres and fine particles is not particularly limited, and may be a device equipped with a very simple mechanism such as a container and a stirring blade, or a general powder mixer capable of shaking or stirring.
  • the powder mixer include powder mixers capable of rocking or stirring, such as ribbon mixers and vertical screw mixers.
  • more efficient multifunctional powder mixers combining a stirring device, such as Super Mixer (manufactured by Kawata Co., Ltd.) and High Speed Mixer (manufactured by Fukae Co., Ltd.), New Gram Machine (manufactured by Seishin Enterprise Co., Ltd.), and SV Mixer (manufactured by Kobelco Eco-Solutions Co., Ltd.), may also be used.
  • a stirring device such as Super Mixer (manufactured by Kawata Co., Ltd.) and High Speed Mixer (manufactured by Fukae Co., Ltd.), New Gram Machine (manufactured by Seishin Enterprise Co., Ltd.), and SV Mixer (manufactured by Kobelco Eco-Solutions Co., Ltd.), may also be used.
  • the adhesion step is a step in which the mixture containing heat-expandable microspheres and fine particles obtained in the mixing step is heated to a temperature above the softening point of the thermoplastic resin constituting the shell of the heat-expandable microspheres, to expand the heat-expandable microspheres and to adhere the fine particles to the outer surface of the shell of the resulting hollow particles.
  • the heating step may be performed using a general contact heat transfer type or direct heating type mixing dryer.
  • the functions of the mixing dryer are not particularly limited, but it is preferable that the temperature is adjustable, that the raw materials are dispersed and mixed, and that a pressure reducing device or a cooling device is provided to accelerate the drying process.
  • the device used for heating is not particularly limited, but examples thereof include a Lödige Mixer (manufactured by Matsubo Corporation) and a Solid Air (Hosokawa Micron Corporation).
  • the heating temperature condition depends on the type of heat-expandable microspheres, but is preferably near the maximum expansion temperature of the heat-expandable microspheres, preferably 70 to 250°C, more preferably 80 to 230°C, and even more preferably 90 to 220°C.
  • Fluorine-containing resins such as vinylidene fluoride-hexafluoropropylene copolymer, vinylidene fluoride-tetrafluoroethylene copolymer, hexafluoropropylene-tetrafluoroethylene copolymer, and ethylene-tetrafluoroethylene; bioplastics such as polylactic acid (PLA), cellulose acetate, polybutylene succinate (PBS), polyhydroxyalkanoate (PHA), and starch resin; silicone-based, modified silicone-based, polysulfide-based, modified polysulfide-based, urethane-based, and a
  • the sealing materials include sealing materials based on acrylic, polyisobutylene, and butyl rubber; liquid components such as emulsions and plastisols based on urethane, ethylene-vinyl acetate copolymer, vinyl chloride, and acrylic; inorganic materials such as cement, mortar, and cordierite; and organic fibers
  • the composition of the present invention can be prepared by mixing at least one selected from heat-expandable microspheres, hollow particles, and microparticle-coated hollow particles with a base component.
  • the composition obtained by mixing at least one selected from heat-expandable microspheres, hollow particles, and microparticle-coated hollow particles with a base component can also be further mixed with another base component to prepare the composition of the present invention.
  • the composition of the present invention may contain, in addition to at least one selected from the group consisting of heat-expandable microspheres, hollow particles, and microparticle-coated hollow particles and a base component, other components depending on the intended use, such as plasticizers, fillers, colorants, high-boiling organic solvents, adhesives, etc.
  • the total content of the heat-expandable microspheres, hollow particles, and hollow particles with fine particles attached thereto is not particularly limited, but is preferably 0.05 to 750 parts by weight per 100 parts by weight of the base component.
  • the total content is 0.05 parts by weight or more, a sufficiently lightweight molded product tends to be obtained.
  • the total content is 750 parts by weight or less, the uniform dispersion of at least one selected from the heat-expandable microspheres, hollow particles, and hollow particles with fine particles attached tends to be further improved.
  • the upper limit of the total content is more preferably 700 parts by weight, even more preferably 650 parts by weight, particularly preferably 600 parts by weight, and most preferably 500 parts by weight.
  • the lower limit of the total content is more preferably 0.1 parts by weight, even more preferably 0.2 parts by weight, particularly preferably 0.5 parts by weight, and most preferably 1 part by weight.
  • the total content is, for example, preferably 0.1 to 700 parts by weight, and even more preferably 0.5 to 600 parts by weight.
  • the molded product of the present invention is obtained by molding the composition described above.
  • the molded product of the present invention may be, for example, a molded article or a coating film.
  • the molded product of the present invention has improved physical properties such as light weight, porosity, sound absorption, heat insulation, low thermal conductivity, low dielectric constant, design, impact absorption, and strength, and also has an excellent appearance.
  • thermodynamical examples of the heat-expandable microspheres of the present invention are described below in detail. However, the present invention is not limited to these examples. In the following examples and comparative examples, “%” means “% by weight” and “parts” means “parts by weight” unless otherwise specified.
  • the heat-expandable microspheres described in the following Examples and Comparative Examples were measured for physical properties and evaluated for performance in the following manner. Hereinafter, the heat-expandable microspheres will sometimes be referred to as "microspheres" for simplicity.
  • the measuring device used was a Microtrac particle size distribution meter (model 9320-HRA) manufactured by Nikkiso Co., Ltd., and the D50 value based on volumetric measurement was taken as the average particle size.
  • Ts expansion beginning temperature
  • Hmax maximum expansion temperature
  • the encapsulation rate (C 1 ) of the blowing agent in the heat-expandable microspheres was calculated according to the following formula.
  • C 1 (weight %) 100 ⁇ 100 ⁇ (W 1 ⁇ W 2 )/1.0 ⁇ C w1 ⁇ /(100 ⁇ C w1 )
  • the water content Cw1 of the heat-expandable microspheres is the value measured by the above-mentioned method.
  • the weight ratio of the hydrocarbon having 5 to 6 carbon atoms in the blowing agent in the heat-expandable microspheres was measured by the head space method of gas chromatography as follows. About 0.05 g of heat-expandable microspheres were weighed into a vial, about 1 g of N,N-dimethylformamide was added to the vial, and the vial was quickly sealed.
  • the sealed vial was then kept at 140°C for 1 hour, after which the gas phase (head space) was sampled with a gas-tight syringe and introduced into GC (GC column: Rxi-62Sil MS (length 30 m, inner diameter 0.32 mm, film thickness 1.8 ⁇ m) manufactured by RESTEK Corporation) to measure the weight percentage of hydrocarbons with 5 to 6 carbon atoms in the blowing agent. Normal hexane was used as the standard sample.
  • the true specific gravity of the heat-expandable microspheres, hollow particles, or fine particle-adhered hollow particles was measured by the following method.
  • the true specific gravity was measured by the immersion method (Archimedes method) using isopropyl alcohol under an atmosphere of an environmental temperature of 25°C and a relative humidity of 50%. Specifically, a 100 mL volumetric flask was emptied, dried, and the weight (WB1) of the volumetric flask was weighed.
  • the weighed volumetric flask was filled with isopropyl alcohol exactly up to the meniscus, and the weight (WB2) of the volumetric flask filled with 100 mL of isopropyl alcohol was weighed.
  • WB2 weight of the volumetric flask filled with 100 mL of isopropyl alcohol was weighed.
  • a 100 mL volumetric flask was emptied, dried, and the weight (WS1) of the volumetric flask was weighed.
  • the weighed volumetric flask was filled with about 50 mL of particle sample, and the weight (WS2) of the volumetric flask filled with the particle sample was weighed.
  • the weight (WS3) of the volumetric flask filled with the particle sample was weighed after the volumetric flask was filled with isopropyl alcohol exactly up to the meniscus without introducing air bubbles.
  • a DMA (DMA Q800 manufactured by TA Instruments) was used as the measuring device, and the prepared sample was pressurized from the top of the aluminum lid at a pressure of 0 to 18 N at a speed of 10 N/min with a pressure bar in an atmosphere of 25°C, and then the pressure was released from 18 N to 0 N at a speed of 10 N/min.
  • the stress at the time of applying a pressure of 18 N was designated as A1
  • the position of the pressure pin was designated as B1.
  • the stress when the pressure pin moved 0.1 mm from the start of decompression was designated as A'1.
  • the compression set (%) of the obtained molded product was measured under conditions of 25% compression at 25° C. for 22 hours according to a method in accordance with JIS K 6262.
  • the measured compression set was judged based on the following evaluation criteria, with a score of ⁇ or higher being considered to be acceptable.
  • Good The compression set is 50% or less, and deformation of the molded product is suppressed.
  • ⁇ Compression set is more than 50%, and deformation of the molded product occurs.
  • the obtained molded product was cut out from the molded product and measured for a test piece measuring 80 mm in length, 25 mm in width, and 2 mm in thickness, and the three-point bending flexibility was evaluated using an Instron universal testing machine (Instron Corporation) according to a method conforming to JIS K7171.
  • the test piece was set on a jig having a pair of supports spaced 64 mm apart, and the bending modulus (MPa) was measured at the center between the supports while pushing the test piece from above at a speed of 1 mm/min. Furthermore, the bending modulus of the base resin was also measured by the above method.
  • the bending strength was calculated from the measured bending modulus of elasticity of the test piece and the bending modulus of elasticity of the base resin according to the following calculation formula (5), and judged according to the following evaluation criteria, with ⁇ or higher being considered as passing.
  • Bending strength bending modulus of molded product / modulus of elasticity of base resin (5)
  • ⁇ The bending strength is 0.90 or more, and deformation of the molded product is further suppressed.
  • Good The bending strength is 0.75 or more and less than 0.90, and deformation of the molded product is suppressed.
  • x The bending strength is less than 0.75, and deformation of the molded product occurs.
  • the b* value of the obtained molded product was measured using a color difference meter (CR-400, manufactured by Konica Minolta, Inc.). This b* value is the b* value in the L*a*b* color system, and the larger this value is, the more yellowed the molded product is.
  • the yellowness was evaluated from the measured b* value of the molded product and judged based on the following evaluation criteria, with a score of ⁇ or higher being considered a pass.
  • ⁇ The yellowing index is less than 3.0, and yellowing of the molded product is suppressed.
  • ⁇ The yellowing index is 3.0 or more and less than 10.0, and yellowing of the molded product is somewhat suppressed.
  • x The yellowing index is 10.0 or more, and yellowing of the molded product cannot be suppressed.
  • Example 1 170 parts of sodium chloride was dissolved in 680 parts of ion-exchanged water, 1.0 part of polyvinylpyrrolidone, 0.05 part of carboxymethylated polyimine Na salt and 55 parts of colloidal silica (effective concentration 20%) were added, and the pH was adjusted to 3.0 to prepare an aqueous dispersion medium.
  • acrylonitrile 2 parts of acrylonitrile, 65 parts of methacrylic acid, 20 parts of methacrylamide, 10 parts of styrene, 160 parts of methacrylonitrile, 1 part of PEG#200 diacrylate, 7 parts of di-2-ethylhexyl peroxydicarbonate (purity 70%), and 65 parts of 2-methylbutane (isopentane) were mixed to prepare an oily mixture.
  • the aqueous dispersion medium and the oil mixture were mixed, and the resulting mixture was dispersed in a homomixer (TK homomixer, manufactured by Primix Corporation) at a rotation speed of 10,000 rpm for 1 minute to prepare an aqueous suspension.
  • TK homomixer manufactured by Primix Corporation
  • the resulting aqueous suspension was transferred to a 1.5 L pressure reactor and purged with nitrogen.
  • the initial reaction pressure was adjusted to 0.35 MPa, and polymerization reaction was carried out at a polymerization temperature of 60° C. for 20 hours while stirring at 80 rpm.
  • the product was filtered and dried to obtain heat-expandable microspheres A.
  • the physical properties of the resulting heat-expandable microspheres were measured and evaluated. The results are shown in Table 1.
  • Example 2 to 9 Comparative Examples 1 to 8
  • heat-expandable microspheres B to P were obtained in the same manner as in Example 1, except for the changes shown in Tables 1 and 2.
  • Comparative Example 3 heat-expandable microspheres were not obtained.
  • the physical properties of the resulting heat-expandable microspheres were measured and evaluated in the same manner as in Example 1. The results are shown in Tables 1 and 2.
  • Example 1 A resin composition obtained by uniformly mixing 970 parts by weight of an olefin-based elastomer (Milastomer 8032NS, manufactured by Mitsui Chemicals, Inc., compression set (23°C/22 hours) 30%, elastic modulus 60 MPa, specific gravity 0.88) and 30 parts by weight of the microspheres A obtained in Example 1 was fed to a hopper of an injection molding machine (J85AD-110H, manufactured by Japan Steel Works, Ltd., mold clamping force 85 tons) and melt-kneaded, and injection molding was performed by the short shot method to obtain a plate-shaped molded product.
  • an injection molding machine J85AD-110H, manufactured by Japan Steel Works, Ltd., mold clamping force 85 tons
  • the molding conditions were as follows: molding temperature: maximum expansion temperature (T max ) of the microspheres A, injection filling time: 1 second, injection speed: 200 mm/sec, mold surface temperature: 30°C, and molded product thickness: 7.0 mm.
  • T max maximum expansion temperature
  • Example 2 to 9 Comparative Examples 1 to 8
  • injection molding was performed under the same conditions as in Example 1 to obtain plate-like molded products.
  • the physical properties of the obtained molded products were measured and evaluated. The results are shown in Tables 1 and 2.
  • the molding temperature was the maximum expansion temperature of each heat-expandable microsphere.
  • the heat-expandable microspheres of Examples 1 to 9 have a thermoplastic resin constituting the shell which is a polymer of a polymerizable component, the polymerizable component containing at least one monomer selected from a carboxyl group-containing monomer, a (meth)acrylic acid ester monomer, a styrene monomer and a (meth)acrylamide monomer, and have a recovery efficiency after compression of more than 0 and not more than 3.5 when heated for 2 minutes at a temperature 20° C. lower than the maximum expansion temperature of the heat-expandable microspheres, and a compression recovery of 65% or more when heated for 2 minutes at a temperature 20° C.
  • the heat-expandable microspheres of the present invention can be used, for example, as a lightweight material for putty, paint, ink, sealant, mortar, paper clay, ceramics, etc., and can also be used together with a base component to produce molded products with excellent sound insulation, heat insulation, heat insulation, sound absorption, etc. by molding using injection molding, extrusion molding, press molding, etc.
  • Microparticle-adhered hollow particle 1 Microparticle-adhered hollow particle 2 Outer shell 3 Hollow portion 4 Microparticle (adsorbed state) 5. Microparticles (embedded and fixed) 6. Shell 7. Foaming agent (core)

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Abstract

Le but de la présente invention est de fournir des microsphères thermo-expansibles capables de produire un article moulé qui n'a pas tendance à se déformer sur le long terme, et l'utilisation des microsphères thermo-expansibles.　La présente invention concerne des microsphères thermo-expansibles comprenant une enveloppe qui contient une résine thermoplastique et un agent moussant qui est encapsulé dans l'enveloppe et qui se vaporise lors du chauffage, la résine thermoplastique étant un polymère d'un composant polymérisable comprenant au moins un monomère choisi parmi des monomères contenant un groupe carboxyle, des monomères d'ester d'acide (méth)acrylique, des monomères de styrène et des monomères de (méth)acrylamide, l'efficacité de récupération après compression lorsqu'elle est chauffée pendant deux minutes à une température 20 °C inférieure à la température d'expansion maximale des microsphères thermo-expansibles étant de plus de 0 à 3,5, et la récupération de compression lorsqu'elle est chauffée pendant deux minutes à une température 20 °C inférieure à la température d'expansion maximale des microsphères thermo-expansibles étant de 65 % ou plus.
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WO2007049616A1 (fr) * 2005-10-27 2007-05-03 Bridgestone Corporation Microspheres a expansion thermique et particules fines creuses, leur procede de production et ensemble pneu et jante
JP2013511583A (ja) * 2009-11-20 2013-04-04 ビーエーエスエフ ソシエタス・ヨーロピア 微小中空球を含有する樹脂発泡体
WO2018025575A1 (fr) * 2016-08-02 2018-02-08 松本油脂製薬株式会社 Particules de résine creuses et utilisation desdites particules de résine creuses

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Publication number Priority date Publication date Assignee Title
WO2007049616A1 (fr) * 2005-10-27 2007-05-03 Bridgestone Corporation Microspheres a expansion thermique et particules fines creuses, leur procede de production et ensemble pneu et jante
JP2013511583A (ja) * 2009-11-20 2013-04-04 ビーエーエスエフ ソシエタス・ヨーロピア 微小中空球を含有する樹脂発泡体
WO2018025575A1 (fr) * 2016-08-02 2018-02-08 松本油脂製薬株式会社 Particules de résine creuses et utilisation desdites particules de résine creuses

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